Apparatus for the treatment and producing of oil-water wells



2,258,615 R'wELLs Oct. 14, 1941. J. F. KENDRICK' APPARATUS FOR THE TREATMENT AND PRODUCING OF OIL -wATE 2 Sheets-Sheet l Filed Feb. 28, l9 38 Isley -wATER wELLs Oct. 14, 1941.

J. F.1KENDR1CK APPARATUS FOR THE TREATMENT AND PRODUCING OF OIL Filed Feb. 28, 1938 2 Sheets-Sheet 2 e E v N UNLaaaER 0 A? a l ER Ffa/v .q Gassaus P055 SURE Sal/RCE equipment V upon the renewal of vvention to provide an improv Patented ct. It, 41941 imitan STATES PATENT OFFICE APPARATUS FOR THE TREATMENT PRODUCIN OF OIL-WATER WELLS John F. Kendrick, Chicago, Ill., assignor to van Machinery Company, a corporation Massachusetts l Sulli- Application February 28, 1938, Serial No. 193,161

1i claims.

This invention relates to apparatus for the treatment and producing of oil iwells, and more particularly to improved apparatus for the treatment and producing of so-called oil-Water wells for the purpose of increasing the proportion of oil in the liquid produced therefrom.

In many oil fields the producing formation is` permeated, prior to commencement of production,l in its lower portions by water which is under pressure. Under such conditions, water` usually ultimately appears in the well discharge, and the quantity of water usually increases with continued production.' until ultimately the wells maybe producing large quantities of liquid of which but a small percentage may be oil. The

total quantity of uid produced is, most frelquently, determined by the capacity of the avail-.- able pumping equipment; and increases in rate of operation, or even in capacity, of pumping the ratio of oil to water. Itis to such wells that commonlydo not increase materially drive seid. It is a further object or-my invention to provide an improved apparatus for treating and producing oil-water wells, utilizing a fluid of lighter specific gravity than the water for forcing down the well the water in the latter, and thereafter producing the well under correlated conditions ofy back pressure and production rate. It is still a furtherobject of my invention to provide an improved apparatus for treating and producing oil-water wells by means of which such wells are subjected to an improved treatmenti-for promoting a restratication in the producing formation. It is yet another object of my invention to provide an improvedapparatus for treating and producing oil-water wells, utilizing a liquid o f lighter specific gravity than the water:

of the well for forcing down the well the water in the present invention has, it is believed, its maximum applicability, but it is to be understood that when an articialwater drive is applied to i a gas-drive eld, there may develop conditions so analogous to those above mentioned as to provide opportunity for a most beneficial application of -this invention in one or another of its embodifments. It should be? further borne `in mind that there maybe other conditions under which the disadvantages of having the oil produced at- `tended byv serious quantities of water -may be overcome by the use .of the'present invention.

'In my copending application Serial No. 193,160 various methods of treating and producing 'oil-g water wells are disclosed and claimed. This present application relates to apparatus for the carrying out of. suchA methods. f

According tothe presentinvention, from a major aspect, apparatus is provided by means of 'which a well may be treated so as to restore, to

oil-water wells. It is another object of my ined apparatus for treating oil-producing formations..5 It is still another object of my invention to provide an improved apparatus for treating the wells of a gasing oil-water wells where the quantity of water l methods is very large.

the latter and thereafter effecting and maintaining a restratiflcationofthe fluids inthe producing formation. It is another object of my invention to provide an improved apparatus for treating and producing oil-water wells, utilizing' gaseous pressure and va suitable liquid cap for forcing down the well the water therein, and subsequently creating and maintaining a. restratiflcation of the fluids in the producing formation. Another object of the invention is to provide an improved apparatus-for establishing a back pressure in an oil-water weil, and producingthe well under the back pressure so provided.

It is, again, an object of my invention to provide an improved apparatus for treating and producvthat must be handled with ordinary production It is another object of my invention to provide an improved apparatus for treating oil-water wells having a relatively high formation pressure in relation to their depth, enabling them to resume production by natural flow. It is a still further lobject of my invention to provide an improved apparatus for to a method which includes the step of forcing dom the well, with a column of lighter liquid,

thevwatenin the. well, and comprising an improved apparatus for effecting the introduction` of the liquid column so utilized.

In the accompanying drawings, in which, to

facilitate understanding, there are presented certain relatively diagrammatic showings of difq ferent embodiments of my invention- Fig. 1 is ,a diagrammatic view of an embodiment utilizable in the practice of my invention when a liquid is the forcing-down agent and the hydrostatic head of the liquid provides the re- V treating and producing oil-water wells according of such liquidmust be forced into the well to drive down the water in the latter.

Fig. 3 is a view showing diagrammatically an embodiment by means of which a liquid may be lintroduced by gravity ow, and cumulatively acting gaseous and hydrostatic pressures effect the forcing-down operation.

Fig. 4 is a diagrammatic view showing illustrative means utilizable,in part; in superimposing gaseous pressures on liquid caps introduced into the well.

Referring to Fig. l, a well I is shown having a casing 2 termina-ting in an impervious stratum I overlying the producing formation 4. bore 5 oi' the well is shown extending for a substantial distance into the formation. Within the casing is a tubing 6 carrying at its lower end a pump 'I which may be of any suitable type and which is herein shown, for purposes of illustration, as of the sucker-rod-actuated type; .and the sucker rod line 8 extends upwardly through the tubing to a point at the surface. The sucker rod is shown as connected to a "horse head A, carried at one end of a walking beam B, pivotally mounted as at C upon a Samson post D. The walking beam is rocked through a pitman E adjustably connected to the multi-holed crank F of a power transmission unit G, which may be ofI a multi-speed type and be driven from a` motor orany other suitable source of power not shown,

'as through the beltl H. The casing head I0 is shown provided with a lineI II controlled by a valve I 2 and having valve-controlled branches I3 and I4, respectively adapted to deliver the casing head gases to any desired point and to permit convenient venting of the casing head pressure if desired. The tubingI 6, as shown, carries at its top a fitting I8 from which a valve# controlled line I'I leads oiT. The line I1 is shown branched, and the branch I8 may lead to a suitable treating system or any other desired point, while the branch I9 is valve-controlled and serves to permit venting of the tubing if desired.

Additional equipment to be used in the practice of my invention is provided, and this may be installed when the well is completed, when the ultimate application of my improved method of treating and producing a well is foreseen, or may be installed at old wells Vat the time' the method is to be applied.

For the introduction of a uid medium for driving down the liquid column in the casing,. there is shown means by which such aliquid agent may be introduced into the tubing, into thel casing, or into both. Introduction through. the tubing presupposes a temporary removal of the pump. or some'other arangement to enable the discharge of the liquid agent through the tubing into the well. Herein a valve-controlled line 2| leads to the top of the tubing, and a valve-controlled line 22 leads to the casing head, while a line2l constitutes a common supply4 line for delivering a liquid agent to the connections 2I and 22. Herein I have shown the supply line 23 leading toa tank 24, which may represent any suitable 'source ofcrude oil.`

It will-.be evident that the piping connections and'controls `shown are wholly diagrammatic and. that they may be widely varied within the scope The 250 crank, and Vchanges may be made4 in the trans-4l well. the casing head pressure will be reduced to the necessary degree, as by opening the valvecause an improved of my invention, and that, for example, single connections with the casing headand the top ofy the tubing migh be'made to serve both supply and discharge functions merely by rearranging l the piping and its fittings.

In other gures treating-agent delivery lines and ,lines for handling the gaseous land liquid discharge of the well are also shown diagrammatically, and throughout the drawings wher# ever similar parts are disclosed like reference numerals will be applied.

During the operation of the well prior to treat-' ment and production thereof according,f tothe method applied with this embodiment of my in vention, the sucker rod line 8 operates the pump 1 and effects vdischarge from the well, through the line I1, of crude oil and water. These liquids may be delivered to any desired point; and the casing head pressure may be maintained high or low, as desired, for example, by adjustment ofv the valve I 2.

This well maybe regarded, forpurposes of illustration, as a rather deep one, having a considerable formation pressure but not `one suiiicient to oder any possibility of production without pumping. Prior to the initiation of treatment of this well, the production of the latter may be assumed to have comprised rather serious quantities of water with some oil, and the pumping equipment, under such circumstances, will have been pressed, perhaps, to near the limit of its capacity to secure enough oil to warrant continued pumping, in view of the high percentage of waterin the well discharge. If such a well is shut down, a column of oil and water will stand comparatively high in the casing, the water component extending from the bottom of the well to a point materially above the top of the producing sands 4, and a mere shutting in of the well would not, in any commercially practicable time, result in any change taking place which would production of oil upon resumed pumping.

A well of the assumed characteristics of the well I requires pumping afteras well as before treatment. Therefore, prior to the introduction of a fiuid to force down the liquid column, the pump 'I and the operating means for the sucker rod line 8 will desirahly be modified and adjusted,

as by reducing the size of the pump plunger and I providing for a less rapid reciprocation of the sucker rod line 8 and shorter strokes of the latter, so that upon the resumption of pumping a much slower discharge rate will be possible. For example, the lower end of the pitman will be connected nearer the axis of rotation of the drive mission between the motor and the power trans- Amission unit or in the gearing of the latter.

controlled-discharge line I4; and then a quantity of crude oil, for example, a quantity which when confined in a column of a cross section equal to that of the casing will exert a force equal to or slightly in excess of the will be iiowed from the source 24 through the line 23 and through theline 22 into the casingto act upon the liquid column standing in the latter. As the crude ou is edged to the wpof the nquid column in the well, the bottom-of the original liquid column will be forced back into the formation; and as more and'more oil enters the casing bottom-hole pressure,

. above the top of only at intervals, and each agissait the column of oil which stands the water column will approach and finally pass below the top of thev oil sands and commence to enter the latter and to displace the water` from the well bore within the sands the lower end of .and from some, at least, of the uppermost waters'ealed oil delivery passages in the sands. The oil column in the casing will not have its upper end move in the casing down to a point below the by gravity flow after a limit fixed by the formation pressure; and it is 1G possible that a considerable time may be required to effeet'the' introduction of the vdesired total quantity of oil and the attainment of a balance between the formation pressure and the pressure exerted by the oil column in the well.

After the o ilhas been introduced, and preferably also after the end of the forcing-down ac- -tion has been reached, thewell may desirably be shut in for a time, as `by closing the valves in the several lines Il, I period varying with the quantity of oilintroduced and with the severity and-duration of the previous water-producing condition. A shut-down of all pumping until the day following the completion of the introductioniof the selected as a convenient, though by no means a fixed, minimum, when this step is regarded as advisable'. This will provide an opportunity for the more definite establishment of restratiflca- 3 tion.

Following the period of complete inactivity, so far as production is concerned-when such a period is provided-a very slow'production may be initiated. The pump will be positioned preferably with its intake above the top of the oil sands; and pumping at a slow rate compared to that which would be sufficient to effect the discharge of the oil component only of the` prior delivery, may be started and maintained fora time to insure still r'nore definitely the effecting of a restratication of the fluids within the producing formation.

Thereafter,` the pumping speed will be in. creased, as by `lengthening the pump stroke through changing the pitmans connection to the crank, until the maximum safe rate of production is attained. In increasing the rate of!Y production, the pumping speed should be increased new rate should .be maintained long enough for sub-surface conditions to become stabilized.

If desired, the rate of production maybe dey liberately increased until water again begins tol appear in substa 'tial quantity. This will enable the experimental determination of the limit beyond which pumping cannot be advantageously pushed. The whole processk maythen be repeated. and theA productionrate formation so obtained, so that` the`maxlmumpracticable quantity of oil may be secured. w

-It will be understood that correlation of the rate of production and of the back pressure-in this instance determined, at least largely, by the guidance as to possible `indicaton in the `volume to be employed.

Instead of introducing the liquid-forcing agent lowering of the-casing head pressure, this agent may be forced into the well by imposing upon it the necessary pressure. Such a procedure will be found advantageous where the formation pressure is high enough, with respect to the depth of the well, to\ permit production by natural flow to be resumed upon the substantial elimination of water fromthe well discharge. An apparatus suited to those conditions may be explained by reference to Fig. 2, disregarding the dotted disclosure of the d suckerzrod and its gland or stuffing box in that figure.

The well and its equipment in Fig. 2 in the main follow the disclosureaof Fig.` 1. 'Provision is oil may be 1, 2i and 22, this shut-in 29 for ses discharge from` made for liquid discharge from the tubing 6 and` the casing head I'Il; for 1 the shutting in of the casing head and for the closing of! of the usual discharge for liquid from the tubing; and for the introduction off'a treating agent into either the tubingor the casing or both. Instead of provision for the gravity flow of crude oil to the connection 2l or 22 in Fig. 2,

, I have shown diagrammatically means for draw- 0 by a pump 32, and means ing crude oil from a storage receptacle 24. through a line 3|, means for placing it under pressure, as

for discharging it, thev line 33, which may supply fluid either, through the line 2l to the tubing 22 to the casing 2.

Where it is to be expected, from the knowledge possessed of the formation pressure and the depth of thefwell, that production by natural flow can be reestablished when the water discharge is substantially eliminated, the pump 1 and its actuating devices may be removed, a' condition which ofthe sucker rod line and its gland in Fig. 2; and prior to the initiation of well .treatment the bottom of the tubing 6 will advantageously be posi tioned above the top of the producing formation 4. The various connections for liquid and gas discharge from the well will then be closed,` .Y

0 the connections 2l and 22 int'o the well, and to Set, with the ining will, of course, be capped r in of the treating liquid 1f production without height-of the column of oil in the casing (which 65 v, production at least mainly oil.

The quantity of crude oil employed in the first may vary widely from t e` step of the process l tentatively suggested, b t

amount hereinabove ordinarily the quantity adequate, and experience at similar wells inthe and knowledge gained same field'will afford casing down to and into the formation;

mentioned will prove- -oil in the casing will drive down in the tubing and inthe casing the liquid columns standing therein. means of suitable capacity to impose the necessary pressure on the introduced liquid to force' it into the well will, of course, be provided. The pressure necessary will be a matter4 of simple calculation, knowing, for example,'the formation pressure or the specific gravity height at which ing head pressure of the liquid columr and the the latter stands when the casis vented. 'mit top or the tubpriorto the forcing pumping it to be effected.

As the columnof oil is forced intothe well, it will progressively displace into the formation the liquidwhich previously stood in the well. When all of that liquid or, yif (water) portion thereof, has been forced below the top of the producing formation, there willv be a continuous column of oil from the top of the i and the effect a junction with the oil in the sands and will displace the water from atleast some of the water-sealed passages and E or through the line-- is suggested by the dotted showing A forcing depthof the we lLthe mean it is stratified, the lower",

, produce a condition where restratication of the iluids in the formation can take place. The well may then, if desired, be shut in by the closing of the necessary valves and allowed 'to stand for a period' morder to promote the initiation of restratiiication. f Thereafter, if a period of very slow production of oil for the purpose of effecting circulation within the formation and the displacement from the oil channels of the water seals therein be desired, it will be possible by throttling the rate of production through the line l1 to maintain the necessary-'back pressure and to hold in check the rate of production to accomplish the desired result. Subsequent production at higher rates will be possible, when this is indicated,'merely` by increasing the rate of oil delivery permitted through theline I1. Should the ratel of production be allowed inadvertently to become too high, or be deliberately allowed to proceed to such a degree as to initiate the return of water to the well discharge, for the purpose of determining the maximum safe rateof production, a reapplication of the process will restore the well to a substantially exclusive oil production.

yIt will be evident that the crude oil or other liquid agent may be forced into the Well either when the latter has a column of liquid of considerable height standing therein (a condition which follows protracted reduction of the casing head pressure), or at a time when the gaseous casing head pressure is high, through the wells having been shut'in for some/time.. Under the latter conditions, the gaseous pressure in the casing will force the treating liquid, as the latter is introduced by the forcing instrumentality into the l well, downwards, and thereby displace the lower 'f .liquid column originallystanding within the well. 'When this has been completed to the necessary degree, -it will be evident that upon resumed production the Well must rely rather llargely upon a gaseous back pressure unless steps are adopted to effect areplacement of the gaseous back pressure, or the combined gaseous and liquid back pressure, by a primarily, at least, liquid back pressure. This can be done readily by allowing the gaseous 'casing head pressure to be` bled off at a .rate so restricted that oil ingress into the Well Ifromlthe formation will cause a column of oil to build up v in the well as the gaseous pressure is reduced, and thereby maintain the desired back pressure upon the formation.

When the depth df the well and the depletion l of the formation pressureare such that production by natural ow will be impracticable, and the embodiment of the invention described with l the aid of Fig. 2 is to be applied, the pumping equipment, whose presence is indicated bythe dotted sucker rod line stuflng box, will, before the liquid agent ls introduced into the well, be modified and readiusted to enable, upon resumed production, slow enough rates of pump operation to bring about the Aneeded restratiiication and to maintain the rate of liquid production within the rate of oil influx into the well. Here it will be understood that the quantity of liquid, e. g. tank oil, will notbe suillcient wholly to Vfill the casing. even when a column of sunlcient height to drive down the water, by its weight, is introduced; and the quantity oftheliquid agent may he varied, as more fully explained in connection with laterv embodiments of the invention, depending upon the relative reliance it is desired t0 place upon hydrostatic and gaseous pressures -for the forcingdown action.

` While but one vessel Aevident that use of a right of the well is shown equipment which can be used for enabling the'introduction, by gravity ow, of a liquid to act upon the top of the liquid column in the well, though the well may be under pressure-and this without the need for means for imposing mechanically upon the liquid a pressure to overcome the pressure against which it is to be introduced. A valve-controlled line 35 is provided to permit delivery of the liquid to be introduced from any suitable source, herein represented by the oil tank 24, to a receptacle or vessel 36 so positioned as to permit gravity flow 'from it into the casing or tubing, or both, respec-l tively through the valve-controlled line valve-controlled line 38, or both. A vent,

31, the suitably valve-controlled, is shown at 39, and means for ow of introducing a pressure to enable gravity the liquid within -the vessel 36 into the to exert, if desired, a superior pressure well, or upon it,

is provided inthe form of the valve-controlledl line 4U, to which casing head pressure `may be admitted through the valve-controlled line 4| leading to the casing head, or to which any suitable gaseous pressure may be delivered from any available source by way of the valve-controlled supply line 42, when a somewhat dierent modification of the invention is desired to be employed.

necessary capacity, or use of a single vessel large enough to hold the entire needed quantity of treating liquid, or use of a small vessel repeatedly, are all within the scope of my invention. Before introduction of the liquid by means of the equipment illustrated in Fig. 3, provision will be made to enable slower displacement of liquid by the pumping equipment. These details need not be described again.

'I'he lines Il and I1 being closed, there Awill exist a pressure within Bthe top of the well (l. e. in the casing head) which will dependupon the formation pressure and the height of the liquid column standing in the well. With each of the valve-controlled lines 31, 38 and 40 closed, the vent line 39 from the vessel 36 will be opened, and the desired vquantity cic gravity than the water in the well will be and casing head V4| tothe top of the vessel 36. As previously indicated, a suitable pressure could be supplied, if preferred, through line 42, for example, from sources such as are described in connection with Fig. 4. Lines 31 and/0F38 will be opened, following, or concurrently with, the application of the needed gaseous pressure on the top of the liquid in the vessel 36, `and the liquid will then ow through the open delivery line wellgand will force down the previous liquid column in the well and move the water in the well to a position below the top of the formation 4. It -wi'li of course be understood that where liquid introduction to the well through the line 38 is to be effected, removal of the pump will have been necessary, unless some arrangement be made to enable liquid to pass the pump valves.

Following the introduction of the necessary quantity o; `liquid downward displacement of the water within Ithe as is illustrated, it wm be number, aggregating theV of liquid of lighter speor lines into the and the completion 4of thev mined. i

Fig. 4 is intended to show, in' the simplest poswell, the ,well may be shut in for a time; vslow pumping to effect acirculation which will clear the water-sealed oil passages carried on for a time; and the `well thereafterproduced at an .appropriatev rate and under the necessary back pressure to confine the production to oil as may be desired. Detailed rediscussion of lthese steps is unnecessary. It should be noted that the quantity of liquid-e. g. `crude oilintroduced may be either sunicient per se wholly to displace the entire previous liquid column in the well or, as more fully considered in connection with another modication, a lesser quantity,'to provide a cap oi the necessary depth, as may be detersible manner, equipment by-means of which, as a iirst step, a cap of a liquid of lower specific .gravity than the water of the well is introduced into the latter and then subjected to gaseous pressure to force it downwardly. Obviously the gaseous pressure may be provided by a com presser-in which event maintenance of a gaseous back pressure by suitable control of the compressor is possible-by a well having a higher casing head pressure than the wellbeing treated, by a gas main containing gas at the requisite pressure, such as the residue lineV froma gasoline plant or a booster station line, or even, under some conditions, by simply shutting in the well and allowing the lpressure which will thereupon build up in the casing head to provide the needed pressure. Other potential sources of gaseous pressure will be evident to those skilled in this r serve to permit introduction into the pipe 45 of a suitable gaseous pressure from some such source as another well, a gas main,etc. A suitable pilot valve vQ, controlling the passage of pressure (through the line R) from the line 45 to the unloading mechanism and venting of the unloading pressure, may be employed to control 'the compressor discharge pressure and maintain it at the height necessaryto effect the forcing- -down operation, or, optionally, atvthe height to provide a desired back pressure.

As in earlier figures, the usual liquid discharge visions for conducting away the casing head gases to a point of use or storage, at I3, and for venting the casing head, at I4, respectively. A pump, actuated in any suitable manner--a walkd ing-beam actuation is indicated for illustrationis shown at 1. The line 45, previously mentioned, constitutes-a means for delivering gaseous pressure from any suitable source to either orboth of the valve-controlledl lines 46 and 41 leading o to the top of the tubing'and to the casing head respectively. The source of supply 24 for the desired quantityof liquid treating-agent is connectible herein through the line 23 and its valvecontrolled branches 2| and 22 to the lines l1 and II respectively, these latter serving as well for liquid ingress lines as for liquid and, gas dis-v charge lines respectively. Obviously many variations of these connections, which are shown for i illustration only, are possible.

The embodiment oi the invention now being described is not limited to, but will be found very desirable under conditions where the bottomhole pressure is comparatively low. Ot course,

5 however, provided higher gaseous pressures be economically available, and the casing and other equipment be able towithstand such pressures, these embodiments may be applied as well to wells having higher bottom-hole pressures.

VAs in the other forms of the invention above described, it will be desirable to reduce the displacement o the pump lunger, to shorten the stroke of the latter, and to arrange for a slower rate 0I pump operation; andalso to alter the V location of the pump intake,if necessary, to inlsure the latters being in liquid and not in gas when the process is applied. Desirably, the necessary changes will be made before the gaseous pressureis applied.

When there is in the well a natural oil cap, and this is augmented by an extraneously introduced cap of liquid oi lowerspeciflc gravity than the water in the wel1,'this will ordinarily greatly improve the results 'of the process; and whenever it is believed that the cap of crude oil upon the column standing in the well prior to the application of my process thereto` isqlikely to be in` adequate or its quantity `is problematical, or

when the use of a lower gaseous pressure is desirable for any reason, or whenv operation under maintenance of a substantial casing head pressure is importantv for any collateral reason, or when it is desired to make use of gaseous pressure accumulating from and within the particu- 35 lar well to be treated as at least in part the pressure agency,vthe extraneous introduction of a cap of liquid will be desirable, though it may not be imperative.

When, if this is to be done, the liquid cap has been introduced into the well, as through the lines 23, 22 and Il, one or the other of the lines 46, l-usually the line leading to the casing head-will be opened, and gaseous pressure will be delivered into the well, say, from therecelver O, or through the line P, to act upon the liquid capl which has been introduced into the latter. By continuing the supply of gaseous pressure so that the casing head pressure will increase, it will be evident that the cap of lighter liquid will be forced down the well and brought into contact with the upper portion, at least, of the formation, and drive the water down into the latter. When shutting in the casing head and building up the pressure from within the well is relied upon, added time must usuallyibe counted on; and when line from the well is indicated at I1, and 'the prothe casing head pressure reaches the magnitude computed to be necessary, when superimposed on the cap oi known height, to overcomethe bottom-hole pressure, it will be evident-that the 50 liquid cap will have been forced down as necesin balance with the apparent pumping head, asl

through control oi its escape, by compressor control, etc.; land subsequent operations will then be similar to those described in the caseV or such other practices.

Where it is desired to replace the gaseous pressure with a back pressure imposed by oil from the formation, after the maintenance for the desired period of the undisturbed state, during 5 which the gaseous pressure is maintained and 4 latiVeIy. `or with gases,

well will be induced'.l The oil' will rise in the well and take the place of the gaseous pressure until all the back pressure is supplied by the column of oil. Thereafte the reinitiation of slow pumping etc., as hereinbefore described may be applied. Generally, the type of back pressure maintenance employed will depend upon the desirability, for collateral reasons, of having a high casing head pressure. If desired, after an oil column has been built up in the well, this may be forced down to insure a more certainfreconditioning, and the shutting in, slow producing, and more rapid producing procedures applied.

It will `be noted that apparatus adapted for I the use of liquids and cumulatively acting liquids and gases have been disclosed.l Apparatus for the maintaining of back presure with liquids supplied from without or produced from within the formation, with liquids and gases acting cumuhas been disclosed. Ultimate controlled production by natural flow under back pressure and by pumping under back pressure have beenv explained. And it will be understood that while I have specifically illustrated a beam-actuated reciprocating pump, rotary or reciprocating pumps, beam or motor actuated pumps all may be used when desired.

This is a continuation-impart-I of my applications Serial No. 96,236, led August 15, 1936, and Serial No. 131,203, filed March 16, 1937.

W'hile there have been specifically described in this application a plurality of embodiments of this invention, it will be understood that these have been disclosed for purposes of-illustration and that the invention may be further modified and practiced in other forms Without departing from its spirit or the scope of the appended claims.

What I4 claim as new and Letters Patent is: Y

1. In combination, in an apparatus for eil'ecting oil delivery from an oil-water well, means for mechanically pumping such a well, means for introducing into such a well a quantity of fluid of lighter specific gravity than the mixture of oil and water therein, and means for vei'i'ecting the building up of a gaseous formation pressure updesire to secure by i on the top of the fluid so introduced to force back into the oil stratum the liquid within the Well, said means for mechanically pumping the well having means for regulating the rate of effective operation thereof.

2. In combination, in an apparatus for eifecting oil delivery from an oil-water well, means for mechanically pumping such a well, and means for introducing into such well a quantity of a liquid of lighter specific gravity than the mixture of oil and water therein while said well remains under pressure including means for storing at the top of such well a and equalizing the pressure upon the top of said liquid with the pressure in said well and permitting gravitational flow oi such liquid into said well to force back into the formation the liquid within the well, said means for mechanically pumping the well having means for adjusting thereafter the rate of eil'ective operation thereof.

3. In combination, in an apparatus i'or effecting oil delivery from an oil-water well, means for pumping such well, means for introducing into quantity of such liquid' such well a quantity of liquid of lighter specific gravity than the mixture of oil and water therein, and means for subjecting the .liquid so introduced to a gaseous pressure from anothery well in which a higher formation pressure exists to' force said liquid into the oil stratum, said means for mechanically pumping for thereafter regulating operation thereof.

v4. In combinatiomin an apparatus for treatthe rate of effective Water of a height suiiicient to overbalance the formation pressure, and means for producing the well under a back pressure with the rate of production and the back pressure correlated to preclude the building 'up of a walter component in the well discharge in excess of a predetermined percent.

5. In combination, in an apparatus for treating and producing an 'oil-water well, means for introducing into the well a quantity of a liquid of lower specific gravity than the water therein sulcient when introduced into the casing to exert a hydrostatic pressure at least equal to the formation pressure, and means for producing the well thereafter under a back pressure provided by the fluid contents of the well and at a rate correlated to such back pressure to preclude a proportion of water inthe well discharge in excess of a predetermined percent.-

6. 'I'he combination set forth in claim 5 together withmeansfor shutting in the well for a period between the'introduction of said liquid and the setting in operation of said producing means.

7. The combination dened in claim 5 in which the means for producing the well is provided with means enabling the subjection of the formation to a comparatively low rate of'oil produc) tion under a back pressure prior vto the establishment of the higher rate of production thereafter applied.

8. In an apparatus for treating and producing an oil-water well, means for effecting reconditioning of the Welland the contiguous producing formation including means for forcing into the well a quantity of crude oil sumcient to fill the well completely full from the casing head to a point below the top of the poducing formation, v

substantial gaseous pressure, means for introducing into the well a cap of a liquid of'lower specific gravity than the water in the well and of such height that the hydrostatic pressure of the cap and the gaseous pressure within the well are eilective to force down the liquid previously standing in the well and displace the water in the well into the producing formation, and meansfor thereafter producing said well, while mainltaining a back pressure thereon, ata rate cor- Trelated to said back pressure to preclude the the well having meansA comprising water in at such a height as when 2,258,615 building up of the water component of the well discharge above a predetermined percentage.

10. In combination, in an apparatus for treating and producing an oil-water well, meansifor introducing into the well a'liquid of lower specic gravity than the water in the well, means for establishing a gaseous pressure in the weil which together with the pressure of the liquid, at least equals formation pressure, means vfor closing the well for a period, and means for producing the well at diierent `rates at least the rst of which is .materially below the previous rate of production of oil alone from the well, said apparatus Aincluding means for maintaining lthe well under apparatus including means for maintaining a a back pressure suiiicient to preclude excessive 15 discharge of water.

back pressure upon the formation throughout pumping at said different rates eiective to' preclude the appearance of an excessive amount of water in the well discharge.

JOHN F. KENDRICK.v 

